Classifications

• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B33/00—Silicon; Compounds thereof
  • C01B33/20—Silicates
  • C01B33/36—Silicates having base-exchange properties but not having molecular sieve properties
  • C01B33/38—Layered base-exchange silicates, e.g. clays, micas or alkali metal silicates of kenyaite or magadiite type
  • C01B33/42—Micas ; Interstratified clay-mica products
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B82—NANOTECHNOLOGY
  • B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
  • B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B33/00—Silicon; Compounds thereof
  • C01B33/20—Silicates
  • C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B33/00—Silicon; Compounds thereof
  • C01B33/20—Silicates
  • C01B33/36—Silicates having base-exchange properties but not having molecular sieve properties
  • C01B33/38—Layered base-exchange silicates, e.g. clays, micas or alkali metal silicates of kenyaite or magadiite type
  • C01B33/40—Clays
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B33/00—Silicon; Compounds thereof
  • C01B33/20—Silicates
  • C01B33/36—Silicates having base-exchange properties but not having molecular sieve properties
  • C01B33/46—Amorphous silicates, e.g. so-called "amorphous zeolites"
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK  ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
  • C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
  • C09C1/40—Compounds of aluminium
  • C09C1/405—Compounds of aluminium containing combined silica, e.g. mica
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/50—Agglomerated particles
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/60—Particles characterised by their size
  • C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/60—Particles characterised by their size
  • C01P2004/64—Nanometer sized, i.e. from 1-100 nanometer
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2004/00—Particle morphology
  • C01P2004/80—Particles consisting of a mixture of two or more inorganic phases
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/60—Optical properties, e.g. expressed in CIELAB-values
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/80—Compositional purity
  • C01P2006/82—Compositional purity water content
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
  • C01P2006/00—Physical properties of inorganic compounds
  • C01P2006/90—Other properties not specified above

Definitions

• the disclosed process involves conducting this general type of reaction in the presence of calculated quantity of sodium sulfate from the outset of the reaction whereby economics are improved and highly refined modifications in the characteristic of the final materials become obtainable.
• the reaction may be varied according to several conditions, such as pH, temperature, concentration, manner of feeding materials and the like whereby to better adapt the new materials to highly specialized needs, such as in rubber compounding and paper production.
• This invention relates to the production of finely divided materials having a variety of uses such as pigments, moisture conditioners, etc., but which are especially useful as rubber reinforcing materials and in paper making.
• the pigments of the invention are produced by the reaction of a water soluble alkali metal silicate with water soluble aluminum salts of strong acids, preferably by the reaction of sodium silicates and aluminum sulfate, according to methods generally related to those described in U.S. Pat. No. 2,739,073.
• the products resulting from the process of this patent, as well as from the similar process of this invention, are, in the sodium form, sometimes described as sodium silico aluminates, sodium alumino silicates, synthetic zeolites, mineral pigments and the like.
• the new products of the present invention are at least comparable in utility to the present best known rubber filler materials, while also having other valuable improved utility in paper production. Therefore, the new products herein, may be readily distinguished from those of the said patent on the basis of rubber suitability criteria alone, and perhaps better so on such basis Since certain highly technical physical properties by which ice they may be distinguished are at least to some extent speculative. Moreover, the process involved herein is significantly different.
• a further improvement in the process of this invention arises in connection with the economics of sodium sulfate recovery, this salt being a by-product of the reaction.
• the present process involves the deliberate addition of sodium sulfate as a part of the reaction medium, as a result of which the sulfate wash liquor contains a much higher concentration of sodium sulfate, i.e., the quantity added plus the amount normally produced in the reaction. Since the quantity of water used for washing the reaction products free of sodium sulfate is the same whether sodium sulfate is added or not, the result is that the wash liquor contains a much higher concentration of this salt and is therefore more economical to recover. As will be seen however, the addition of sodium sulfate has significance other than this advantage.
• Another advantage of the invention which fiows directly from reacting the materials from the inception of the reaction in the presence of sodium sulfate is that the re sulting product is more uniform throughout a particular batch. It appears that sodium sulfate has a pronounced efiect upon the nature and size of the aggregate, the tendency being toward the formation of smaller aggre gates, together with an increase in surface area and oil absorption properties. It is thought possible that this advantage is due basically to the more uniform chemical reaction conditions of the present process in contrast to prior processes.
• the basic reaction heretofore known produces sodium sulfate. As the reaction proceeds over a period of time, sodium sulfate, starting from zero quantity, builds up to the total amount formed at the conclusion of the reaction.
• the reaction environment is quite different at the beginning as compared with the environment after several minutes, and it constantly changes until complete.
• the effects of this salt are present from the beginning so that a period of time does not exist when the effects are completely absent and there is no period of time when there is less than the optimum amount of the salt.
• the optimum amount, as well as useful minimum amounts, are a contribution of this invention.
• the products of this invention are similar to those heretofore produced following the procedures described in U.S. Pat. No. 2,739,073.
• these products are compositions essentially consisting of alkali metal, aluminum and silicon oxides, obtained in extremely small particle sizes, as very fine precipitates, by suitable commingling and reacting together, at very low concentrations, dilute aqueous solutions of an alkali metal silicate and a water soluble aluminum salt such as aluminum sulfate, aluminum chloride, aluminum nitrate or ammonium alum.
• the precipitated pigment particles are substantially all less than one micron in diameter, and they average less than one-half micron in diameter. In the main the particles range from about 0.02-0.5 micron. Moreover, they are characterized by extraordinary brightness and by other qualities as hereinafter described which make them exceptionally valuable for uses of the nature indicated above.
• the basic reaction may be selectively directed to produce specialized forms of sodium silico aluminates.
• specialized forms is meant that the present invention permits one to tailor the end product according to the most desirable form for use in a particular environment.
• a reinforcing material for use in rubber shoe soles, heels, and the like of the highest quality is desired, certain overall conditions are found to respond to provide an optimum set of performance characteristics.
• the present invention provides such products of highly improved character.
• the rubber industry not only requires reinforcing materials having very particular performance characteristics, but also the economic aspects of the final rubber producing process must not be affected adversely by the materials added.
• the aspect of the present invention having to do more particularly with rubber reinforcement in the field of tires involves several characteristics similar to those required in the shoe field; but certain performance characteristics are required in tires which differ significantly. In other words, the most desirable tire pigment is not necessarily equally suitable in the shoe art.
• the present invention provides reinforcing material for tires which are tailored to fulfill specific needs and which are superior in performance.
• pigments are to be employed as fillers in paper making, certain somewhat differ characteristics are desirable. Although any of the pigments produced according to this invention may be employed as paper fillers with advantages over previous fillers, those that are produced under certain controlled conditions are more especially desirable because of greater improvement in strike-through performance. This is especially im portant in low grade paper stock, such as newsprint.
• the sodium sulfate must be present from the beginning of the reaction in a minimum amount, it may be present in quite a large quantity without deleterious effects, at least insofar as the objects of this invention are concerned.
• the present invention teaches a range of sodium sulfate conditions which produces worthwhile results.
• the rate of feed of the aluminum sulfate provides a further means of control upon the nature of the end product. Still further as regards products having special utility in the shoe industry, such products may be obtained by varying the approach to the reaction somewhat from that which has just been described.
• the reaction may be conducted with the view to obtaining such improved products varying only slightly in character by establishing a sodium silicate-sodium sulfate reaction medium composed of as little as approximately 50% of the total of such materials calculated to be necessary in the reaction in relation to the aluminum sulfate, the remainder of the sodium silicate-sodium sulfate solution being fed to the reaction mass as a stream (or streams) concurrently with a separate stream of aluminum sulfate.
• some variation of the rate of feed of aluminum sulfate and other process modifications are possible within limits without destruction of desirable qualities of the end product. Modification of the conditions just described, i.e., manner of commingling the reactants, leads to the production of slightly different products; however, all of the products are improved in one respect or another over those previously known for use in the same environment.
• the reaction is conducted in a slightly different manner since the desired differences in the products are significant and demonstrable in use.
• a relatively smaller portion of the pre-calculated amounts of sodium silicate and sodium sulfate (usually herein fed as a single combined stream) is employed as the reaction medium, the remainder of such pre-calculated amount constituting the sodium silicate-sodium sulfate feedstream, which is fed simultaneously with a stream of aluminum sulfate.
• the properties that are produced according to this technique are found to appear increasingly prominently in relation to the smallness of the quantity of sodium silicate-sodium sulfate in the solution which provides the reaction medium.
• the critical point is in relation to the minimum quantity of sodium sulfate which is desirable to be present initially as a part of the reaction medium.
• the exact amount delivered to form the reaction medium will vary. However, for example, in performing the reaction within the preferred conditions herein, approximately of the total quantity of silicate and sodium sulfate are employed to constitute the reaction medium to which the remainder of the reactants are delivered over a period of time; and, while still obtaining a product of improved quality for the particular use, as much as approximately 50% of the total sodium silicate-sodium sulfate pre-calculated amount may be delivered to form the reaction medium.
• the sodium sulfate-sodium silicate does not necessarily require to be admixed and fed in as a single stream to provide the reaction medium. Instead, the quantity of sodium sulfate may be fed separately as a stream; or the total; or any part of the total quantity thereof, may be predelivered to the water mass in advance of delivery of the reacting chemicals. Moreover, if desired, the sodium sulfate may be fed to the reaction medium with the aluminum sulfate, a minimum quantity of the sodium sulfate having been pre-delivered to the reaction zone.
• a further significant aspect of the process concerns the pH of the final pigment end products.
• pigments which are produced by conducting the process within the range of operating techniques above described, and which have improved properties over those heretofore known, have a pH value of from about 7 to 11.
• pigment pH has a definite relation to the suitability of the pigments for use in the several different environments generally discussed above. More particularly, it has been discovered that when a pigment is produced having a pH within the range of about 7.2 to 8.5, more especially and preferably, within the range of about 7.5 to 8, such pigments exhibit certain characteristics or properties rendering them more useful in paper and in the production of rubber tires.
• Pigments having a pH within the range of about 7 to 8 are found to exhibit certain characteristics or properties rendering them of improved usefulness in the shoe industry in the production of soles, heels and the like. Therefore, looking to the object of providing the tailor-made products of the present invention, it is an aspect of the invention to control the pH of the ultimate product.
• pH conrol involves particular adjustment to the initial reaction leading to pigment precipitation.
• the reaction is conducted such that the final pigment slurry resulting from the reaction falls within particular levels according to the desired ultimate pH of the pigment.
• the reaction is controlled to provide a final slurry pH falling between about 5.5 to 9.5, more particularly and preferably a pH of about 5.8 to 7.0.
• the final slurry may fall within the same pH range, that is to say about 5.5 to 9.5, however, more particularly and preferably, the final slurry pH is controlled such that its pH is about 5.8 to 6.0.
• the final slurry pH is directly related to the sulfate ion content of the slurry and this i readily controlled by adjustment of the quantity of aluminum sulfate which is fed to the reaction. That is to say, since the pH of the final slurry is desired to fall on the acid side, then slightly more aluminum sulfate than needed is provided for reaction with the sodium silicate. Similarly, if a lower slurry pH is desired, a slightly higher quantity of aluminum sulfate is provided. It may be remarked that the higher pH pigments are seen to afford slightly shorter scorch times in the rubber compounding process. On the other hand, as the pigment pH increases towards a higher value, the stiffness quality of the rubber end product begins to degrade slightly.
• the desired pigment product pH level is very readily controlled or established by adjusting the reaction medium to the acid side with a slight excess of aluminum sulfate. It is now desired to discuss the matter of pH from another standpoint also having a bearing on the nature of the end products. This additional standpoint has to do with the pH of the reaction medium over the period of time during which the precipitation reaction is taking place. This period of time may be varied widely; however, in general, the reactions extend from approximately 20 to approximately 40 minutes for completion, aside from ageing time before the slurry is filtered. Thus, in discussing precipitation pH, will be understood that such is in relation to conditions occurring in such periods of time as well as other times which may be adopted for carrying out the precipitation reaction.
• the precipitation pH level exerts a marked effect upon the nature of the particles which make up the final pigment end products.
• the reaction conditions are maintained on the basis of pre-established feed rates of the aluminum sulfate.
• the higher the feed rate for aluminum sulfate the lower the precipitation pH and vice versa.
• alum feed rate has very little effect on pH until that quantity is used up in the reaction.
• the general reaction involving sodium silicate and aluminum sulfate may be carried out over a wide temperature range.
• the presence of the minimum quantity of sodium sulfate throughout the reaction according to this invention requires no particular changes in established temperature conditions.
• the improved characteristics of the pigments, which effect their increased utility in the rubber compounding processes wherein the scorch time is markedly reduced result where the reaction as heretofore described is conducted at a temperature within the range of about 70 F. to about 180 F. or higher, although there is no particular advantage in higher reaction temperatures. All things considered in rendering the reaction more practical, a more suitable temperature range is from about 115 F. to about 165 F.
• the aluminum sulfate and sodium silicate streams are adjusted to provide a reaction temperature falling within the range of about to about 150, preferably about to In all cases, however, it has been found to be advantageous to feed the aluminum sulfate stream to the reaction at a temperature as high as this range and preferably at a temperature of at least 130 up to about F. depending upon the objective.
• the importance of the aluminum sulfate temperature control is thought to be related to modifications occurring in the surface chemistry of the particles of pigments produced.
• certain of the properties of the pigments of the present invention are thought to occur according to the coordination of aluminum with silica, precipitation of the pigment during the reaction being achieved via aluminum sulfate. It is thought that such precipitation and coordination depend significantly upon the uniform availability of aluminum ions in an acidic media. Such availability itself is related to the dissociation and acidity of the aluminum sulfate, which is temperature related. It may be, therefore, that the recommended temperature control of the aluminum sulfate feed stream leads to the production of pigments having a higher uniformity of surface chemistry characteristic, the reaction environment being such as to afford especially uniform precipitating and surface coordinating conditions.
• a sodium silicate-sodium sulfate solution is prepared containing the silicate within the range of about 0.50 to 3.0 lbs./ gal. and sodium sulfate is added thereto in an amount of from 1 to 10% by weight of such silicate solution.
• sodium sulfate is added thereto in an amount of from 1 to 10% by weight of such silicate solution.
• sodium sulfate is supplied in a greater amount, that is to say towards the upper part of the l to 10% range.
• more concentrated silicate solutions are combined with a lower quantity of sodium sulfate.
• the process is carried out by feeding separate streams of the thus prepared sodium silicate-sodium sulfate solution and the aluminum sulfate solution, as is presently preferred in the production of tire pigments and newspaper pigments especially suitable concentrations for sodium silicate are found to lie within the range of about 1.4 to 1.6 lbs./gal., usually about 1.5 lbs/gal.
• the amount of sodium sulfate applied is about 5% by weight of the sodium silicate solution.
• Such stream is delivered to a reaction chamber containing a volume of fresh water, such volume being from about 0.4 to about 1.2 gallons of water/lb. of silicate, preferably about 0.6 to 1.
• the concentration of the prepared sodium silicate solution is 9 preferably within the range of about 0.6 to 0.8 lb./gal., usually about 0.70 lb./gal.
• Sodium sulfate in this instance is employed on the basis of about 3% by weight of the silicate solution.
• the total or a major quantity of the calculated amount of sodium silicate and sodium sulfate is provided as a reaction medium (such being the preferred approach in producing materials of higher usefulness in shoe soles and the like)
• the objective is to produce materials better suited for such as the tire and paper industries, longer commingling times are found to be more desirable.
• reaction medium containing less than 50% of the calculated total quantity of sodium silicate and sodium sulfate, as for example 10%
• the total of the aluminum sulfate and the remaining quantity of sodium silicate-sodium sulfate solution be commingled in the reaction medium by delivering separate streams thereto over a period not less than about 25 minutes, preferably 35-40 minutes.
• the concentration of aluminum sulfate it will be understood that such is in relation to the total quantity of water which may be introduced into the process as generally taught and contemplated to be suitable as hereinbefore indicated, other conditions being taken into account. Accordingly, having in mind concentrations which are suitable in relation to the other suitable conditions herein discussed whereby the various products are obtainable, it has been found that the concentration of the aluminum sulfate stream may vary considerably, however, preferably as a practical matter, not less than about 0.1 and not more than about 3.5 lbs./ gal.
• aluminum sulfate concentrations of about 1.2 to about 1.6, specifically about 1.4 lbs./-gal. are particularly applicable.
• a more suitable concentration relative to other suitable conditions for tire reinforcing, paper and the like is from about 2.2 to 2.8 lbs./-gal., more particularly about 2.5 lbs/gal.
• the quantity of aluminum sulfate actually fed to the precipitation reaction is such as to provide a final slurry having a pH level consistent with the pH of the desired end product.
• the reaction vessel itself should be equipped with heating means, for example a steam jacket, in order to maintain the desired reaction temperature; also, it should have adequate agitating mean to produce a strong backflow on the body of liquid and thus avoid zones of high concentration of the incoming reactants. It is desirable to bring the reactants together so as to produce an instantaneous reaction of all material being fed to the fullest extent reasonably possible, as such promotes uniformity of the resulting products.
• Storage vessels equipped with heating means are provided for the reactants, they being connected to the reaction vessel thru lines fitted with flow control means.
• the reaction vessel is equipped with an outlet line leading to a filter which may be of the rotary-string release type, where the precipitate is water washed to remove sodium sulfate as a liquid, the-latter liquor being sent to storage. A portion of this sulfate liquor is utilized in succeeding production as the source of the minimum amount of sodium sulfate needed according to this invention.
• the filter cake being thixotropic requires to be liquefied and for this purpose a tank is required equipped with a suitable beater. The mass is dried in conventional spray drying equipment.
• EXAMPLE 1 The reaction vessel is charged with gals. of water and a sodium silicate (Na O2.5 SiO )-sodium sulfate solution of a silicate concentration of 1.6 lbs./gal. and a sodium sulfate concentration of 5% by weight of the silicate is delivered thereto at a rate of 0.196 g.p.m. (gallons per minute) for one minute.
• the temperature of the resulting reaction solution is established and maintained at 160 F. Alurn in concentration of 2.6 lbs/gal. at a temperature of 160 F. is delivered to the reaction volume, the agitator being first started, at a rate of 0.066 gaL/min.
• the resulting cake being solid (thixotropic), is delivered to a heater and fluidized after which it is spray dried at an outlet pigment temperature of about 220 F. to a moisture content of 5%.
• the resulting dry pigment has a pH of 8.5 and the mass is composed of extremely fine particles relatively few of which are larger than 0.5 micron.
• Example Number Volume of reaction water gallons 10 10 10 10 10 Silicate feed rate, including Na2SO4, gals./m.in O. 196 0.196 0.196 0. 196 0. 196
• Initial silicatesulfate feed-time mlns- 1 7. 8 19. 5 31. 2 39. 0 Silicate-sulfate addition time, mins. 38 31. 2 19. 5 7. 8 0 Silicate concentration, lbs .lgal 1. 6 1. 6 1. 6 1. 6 1. 6 1. 6 Salt concentration in silicate, percent- 5 5 5 5 5 Alum concentration, lbsJgal 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 2. 6 Concentration silicate in reactor before alum starts, 1 0. 03 0. 0. 44 0. 61 0.69 Alum rate, gal/min 0. 066 0. 076 0. 102 0. 159 0.
• Example Number Volume of reaction water gallons 10 10 1O 10 Silicate feed rate, including Na SO gals lmi O. 196 0. 196 0. 196 0. 196 Initial silicate-sulfate ieed-time, mins- 39 4 39 4 Silicate-sulfate addition time, ruins... 0 35 0 35 Silicate concentration, lbs/gal 0. 71 1. 0 0. 71 1. 5 Silicate mol ratio 3. 3 3. 3 2. 0 2. 0 Salt concentration in silicate, percent 6. 0 10. 0 3. 0 8 Alum concentration, lbs/gal 1. 4 2. 0 1. 4 2. 5 Concentration silicate in reactor before alu'n starts, lb gal 0. 71 0. 07 0. 71 0. 11 Alum rate, gal/min 0. O. 057 O.
• Examples 1-14 a sodium silicate of the weight ratio Na O:2.5 SiO was employed.
• Examples 15 and 16 indicate procedures and conditions wherein the silicate weight ratio is according to the formula Na O:3.3 SiO
• Examples 17 and 18 illustrate procedures and conditions wherein the silicate has the ratio of Na O:2.0 SiO
• Examples 15 to 18 the results obtainable are entirely similar to results obtained in the use of the 2.5 ratio silicate carried out according to this invention.
• the invention may be practiced utilizing a Wide range of silicates, more particularly within the range of about 1.5 to 3.5 SiO :Na O by weight.
• test data respecting initial, minimum and maxi- 15 mum viscosity and also scorch time, was derived utilizing the Monsanto Oscillating-Disk Rheometer.
• reaction temperature is maintained at least F. and said aluminum sulfate is delivered at a temperature of at least F.
• reaction temperature is maintained at least as high as 125 F. and said aluminum sulfate is fed at a temperature of at least 130 F.

Landscapes

• Chemical & Material Sciences (AREA)
• Organic Chemistry (AREA)
• Inorganic Chemistry (AREA)
• Engineering & Computer Science (AREA)
• Nanotechnology (AREA)
• Composite Materials (AREA)
• Life Sciences & Earth Sciences (AREA)
• General Physics & Mathematics (AREA)
• Materials Engineering (AREA)
• Crystallography & Structural Chemistry (AREA)
• Physics & Mathematics (AREA)
• Dispersion Chemistry (AREA)
• Condensed Matter Physics & Semiconductors (AREA)
• General Life Sciences & Earth Sciences (AREA)
• Geology (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Paper (AREA)
• Pigments, Carbon Blacks, Or Wood Stains (AREA)
• Silicates, Zeolites, And Molecular Sieves (AREA)
• Solid-Sorbent Or Filter-Aiding Compositions (AREA)
• Furniture Connections (AREA)

Applications Claiming Priority (1)

Publications (1)

Family

ID=24937216

Family Applications (1)

Country Status (15)

Cited By (22)

Families Citing this family (2)

• 1968
  • 1968-05-21 US US730892A patent/US3582379A/en not_active Expired - Lifetime
• 1969
  • 1969-05-14 CA CA051532A patent/CA924078A/en not_active Expired
  • 1969-05-14 GB GB1265898D patent/GB1265898A/en not_active Expired
  • 1969-05-19 BR BR208928/69A patent/BR6908928D0/pt unknown
  • 1969-05-20 LU LU58668D patent/LU58668A1/xx unknown
  • 1969-05-20 SE SE07122/69A patent/SE350763B/xx unknown
  • 1969-05-20 ES ES367460A patent/ES367460A1/es not_active Expired
  • 1969-05-20 NO NO02060/69A patent/NO126612B/no unknown
  • 1969-05-20 FI FI1499/69A patent/FI53443C/fi active
  • 1969-05-21 FR FR6916467A patent/FR2009019A1/fr not_active Withdrawn
  • 1969-05-21 BE BE733358D patent/BE733358A/xx unknown
  • 1969-05-21 DE DE1925868A patent/DE1925868C3/de not_active Expired
  • 1969-05-21 JP JP44038816A patent/JPS4928358B1/ja active Pending
  • 1969-05-21 NL NL6907758A patent/NL6907758A/xx unknown
  • 1969-05-21 DK DK274569A patent/DK144368C/da not_active IP Right Cessation

Also Published As

Similar Documents